Fluid catalytic cracking catalyst for organic pollutant wastewater treatment
A method of removing an organic pollutant from water that includes contacting contaminated water with a filtration membrane including sorbent particles of a spent fluid catalytic cracking catalyst (FCC) that includes a porous aluminosilicate material, and a carbonaceous material disposed on a surface of the porous aluminosilicate material, and a polymer support, to form a contaminated membrane, and collecting a purified water. The sorbent particles include 8.0-50.0 atom % carbon, based on a total number of atoms of sorbent particles, and the organic pollutant is at least one selected from the group including a dye, a phenol, a polycyclic aromatic hydrocarbon, an herbicide, a pesticide, and a persistent organic pollutant.
1 . A method of removing organic pollutants from water comprising the steps of:
providing a filtration membrane;
the filtration membrane comprising:
a porous polymer support;
sorbent particles of a spent fluid catalytic cracking catalyst that include a porous aluminosilicate material formed as a layer on the porous polymer support defining an upstream surface and a downstream permeate surface, wherein the sorbent particles comprise 8.0 to 50.0 atom % carbon, based on a total number of atoms of sorbent particles;
a carbonaceous material disposed on the upstream surface of the porous aluminosilicate material; and
a silica coating disposed on the upstream surface of the porous aluminosilicate material and a surface of the carbonaceous material;
flowing water contaminated with at least one organic pollutant that is selected from the group consisting of: a dye, a phenol, a polycyclic aromatic hydrocarbon, a herbicide, a pesticide, a persistent organic pollutant, and combinations thereof, through pores of the filtration membrane, producing a permeate with a reduced organic pollutant concentration and a contaminated membrane.
2 . The method of removing organic pollutants from water of claim 1 , wherein the porous aluminosilicate material is a USY zeolite.
3 . The method of removing organic pollutants from water of claim 1 , wherein the sorbent particles comprise 18.0 to 30.0 atom % carbon, based on a total number of atoms of sorbent particles.
4 . The method of removing organic pollutants from water of claim 1 , wherein the sorbent particles have a silicon to aluminum atomic ratio of 2.70 to 4.50.
5 . The method of removing organic pollutants from water of claim 1 , wherein the sorbent particles have:
a BET surface area of 115 to 150 m 2 /g;
a pore volume of 0.1500 to 0.1850 cm 3 /g, and
a mean pore size of 4.75 to 6.00 nm.
6 . The method of removing organic pollutants from water of claim 1 , wherein the sorbent particles have a mean particle size of 25 to 400 μm.
7 . The method of removing organic pollutants from water of claim 1 , wherein the porous polymer support is a polypropylene support.
8 . The method of removing organic pollutants from water of claim 1 , wherein the porous polymer support has a mean pore size of 0.10 to 0.50 μm.
9 . The method of removing organic pollutants from water of claim 1 , wherein the carbonaceous material is a fluid catalytic cracking coke.
10 . The method of removing organic pollutants from water of claim 1 , further comprising recovering the organic pollutant by contacting the contaminated membrane with an elution solvent to form a contaminated solvent comprising the organic pollutant; and collecting the contaminated solvent.
11 . The method of removing organic pollutants from water of claim 10 , wherein the elution solvent is at least one elution solvent selected from the group consisting of 2-propanol, acetone, methylene chloride, chloroform, methanol, ethyl acetate, and combinations thereof.
12 . The method of removing organic pollutants from water of claim 1 , wherein the organic pollutant is at least one organic pollutant selected from the group consisting of isoprocarb, atrazine, primicarb, penconazole, chlorfenapr, mefenacet, and combinations thereof.
13 . The method of removing organic pollutants from water of claim 1 , further comprising:
forming the filtration membrane by washing a spent fluid catalytic cracking catalyst with an alcohol having 1 to 5 carbon atoms to form an untreated aluminosilicate material; and
disposing the untreated aluminosilicate material on the porous polymer support.
14 . The method of removing organic pollutants from water of claim 1 , further comprising:
forming the filtration membrane by washing a spent fluid catalytic cracking catalyst with an alcohol having 1 to 5 carbon atoms to form an untreated aluminosilicate material;
calcining the untreated aluminosilicate material at 500 to 750° C. for 1 to 12 hours to form a treated aluminosilicate material; and
disposing the treated aluminosilicate material on the porous polymer support.
15 . The method of removing organic pollutants from water of claim 1 , further comprising:
forming the filtration membrane by washing a spent fluid catalytic cracking catalyst with an alcohol having 1 to 5 carbon atoms to form an untreated aluminosilicate material;
solvothermally treating a coating mixture comprising the untreated aluminosilicate material and an organosilane at 75 to 125° C. for 8 to 48 hours to form an intermediate; and
calcining the intermediate at 500 to 750° C. for 1 to 12 hours to form a coated aluminosilicate material; and
disposing the coated aluminosilicate material on the porous polymer support.
16 . The method of removing organic pollutants from water of claim 15 , wherein the organosilane is tetraethoxysilane.
17 . The method of removing organic pollutants from water of claim 15 , wherein the coating mixture has a weight ratio of the untreated aluminosilicate material to the organosilane of 2:1 to 1:2.